[go: up one dir, main page]
More Web Proxy on the site http://driver.im/

MY160806A - Primary reformer for reduced nitric oxide formation - Google Patents

Primary reformer for reduced nitric oxide formation

Info

Publication number
MY160806A
MY160806A MYPI2011005615A MYPI2011005615A MY160806A MY 160806 A MY160806 A MY 160806A MY PI2011005615 A MYPI2011005615 A MY PI2011005615A MY PI2011005615 A MYPI2011005615 A MY PI2011005615A MY 160806 A MY160806 A MY 160806A
Authority
MY
Malaysia
Prior art keywords
flue gas
gas
tunnels
firing chamber
firing
Prior art date
Application number
MYPI2011005615A
Inventor
Oliver Meissner
Von Trotha Thilo Dr
Original Assignee
Thyssenkrupp Uhde Gmbh
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Priority claimed from DE102009030480A external-priority patent/DE102009030480B3/en
Priority claimed from DE102010024539.9A external-priority patent/DE102010024539B4/en
Application filed by Thyssenkrupp Uhde Gmbh filed Critical Thyssenkrupp Uhde Gmbh
Publication of MY160806A publication Critical patent/MY160806A/en

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/32—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air
    • C01B3/34—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents
    • C01B3/38—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts
    • C01B3/384—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts the catalyst being continuously externally heated
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/32—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air
    • C01B3/34—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents
    • C01B3/38—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
    • B01J8/06—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds in tube reactors; the solid particles being arranged in tubes
    • B01J8/062—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds in tube reactors; the solid particles being arranged in tubes being installed in a furnace
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008—Controlling the process
    • B01J2208/00017—Controlling the temperature
    • B01J2208/00504—Controlling the temperature by means of a burner
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008—Controlling the process
    • B01J2208/00017—Controlling the temperature
    • B01J2208/0053—Controlling multiple zones along the direction of flow, e.g. pre-heating and after-cooling
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/02—Processes for making hydrogen or synthesis gas
    • C01B2203/0205—Processes for making hydrogen or synthesis gas containing a reforming step
    • C01B2203/0227—Processes for making hydrogen or synthesis gas containing a reforming step containing a catalytic reforming step
    • C01B2203/0233—Processes for making hydrogen or synthesis gas containing a reforming step containing a catalytic reforming step the reforming step being a steam reforming step
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/08—Methods of heating or cooling
    • C01B2203/0805—Methods of heating the process for making hydrogen or synthesis gas
    • C01B2203/0811—Methods of heating the process for making hydrogen or synthesis gas by combustion of fuel
    • C01B2203/0816—Heating by flames
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00—Technologies relating to chemical industry
    • Y02P20/10—Process efficiency
    • Y02P20/129—Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • General Health & Medical Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Inorganic Chemistry (AREA)
  • Hydrogen, Water And Hydrids (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)

Abstract

METHOD FOR CATALYTIC PRIMARY REFORMATION OF HYDROCARBONS WITH STEAM AT ELEVATED PRESSURE BY MEANS OF A REACTOR ACCORDING TO CLAIM 1, COMPRISED OF A SPLIT TUBE SYSTEM AND A FIRING CHAMBER (1), WHEREIN IN THE SPLIT TUBE SYSTEM WHICH CAN BE FILLED WITH A CATALYST MATERIAL, HYDROCARBONS TO BE REFORMED ARE CONVERTED BY MEANS OF WATER STEAM TO SYNTHESIS GAS, AND WHEREIN THE SPLIT TUBE SYSTEM IS HEATED BY A PLURALITY OF FIRING FACILITIES EACH ARRANGED BETWEEN THE SPLIT TUBES AND WHICH ARE COMPRISED OF A PLURALITY OF BURNERS (3) ARRANGED IN SERIES, WITH THE BURNERS (3) BEING ABLE TO GENERATE MAINLY DOWNWARDLY DIRECTED FLAMES, AND WHEREIN THE RELEVANT FIRING FACILITIES ARE SUPPLIED WITH FUEL GAS AND AIR, WITH THE AIR BEING WITHDRAWN FROM THE RELEVANT FEEDERS, AND WHEREIN THE FLUE GAS THUS EVOLVING PASSES THROUGH THE FIRING CHAMBER (1) FROM TOP TO BOTTOM AND ENTERS IN THE LOWER AREA OF THE FIRING CHAMBER (1) INTO MAINLY HORIZONTALLY ARRANGED FLUE GAS TUNNELS (4) EXTENDING IN PARALLEL TO EACH OTHER AND PERPENDICULAR TO THE VERTICAL SPLIT TUBES AND BEING ALLOCATED TO ONE FIRING FACILITY EACH, SAID FLUE GAS TUNNELS (4) BEING MADE OF CERAMIC MATERIAL, AND SAID FLUE GAS ENTERING THROUGH APERTURES IN THE LATERAL WALLS OF THE FLUE GAS TUNNELS (4), AND WHEREIN THE FLUE GAS AT THE EXIT OF THE FIRING CHAMBER (1) IS PASSED INTO DEVICES THAT ARE UTILIZED FOR HEAT RECOVERY, AND WHEREIN IN EVERY SINGLE FLUE GAS TUNNEL (4) AN ADDITIONAL GAS IS FEEDED THROUGH MEANS FOR FEEDING INTO THE TUNNEL’S FRONT SIDE, IN FLUE GAS FLOW DIRECTION, WHEREIN THE GAS CONTAINING OXYGEN AND A NON-COMBUSTIBLE GAS, SO THAT THE ADDITIONAL GAS PASSES THE FLUE GAS TUNNELS (4) OVER THE ENTIRE LENGTH OF THE FIRING CHAMBER (1), WITH THE VOLUME OF THE ADDITIONAL GAS PASSED INTO THE FLUE GAS TUNNELS (4) BEING REGULATED. (FIG. 5)
MYPI2011005615A 2009-06-24 2010-06-24 Primary reformer for reduced nitric oxide formation MY160806A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE102009030480A DE102009030480B3 (en) 2009-06-24 2009-06-24 Reactor for catalytic primary reformation of hydrocarbons with steam, comprises reformer tube system used as reaction chamber, and burning chamber, where the reformer tube system has vertical tubes, feeding devices and discharging devices
DE102010024539.9A DE102010024539B4 (en) 2010-06-21 2010-06-21 Primary reformer with variable flue gas flow

Publications (1)

Publication Number Publication Date
MY160806A true MY160806A (en) 2017-03-31

Family

ID=43259838

Family Applications (1)

Application Number Title Priority Date Filing Date
MYPI2011005615A MY160806A (en) 2009-06-24 2010-06-24 Primary reformer for reduced nitric oxide formation

Country Status (15)

Country Link
US (1) US8882866B2 (en)
EP (1) EP2445830B1 (en)
CN (2) CN106395745A (en)
BR (1) BRPI1015230A2 (en)
CA (1) CA2763108A1 (en)
CO (1) CO6470869A2 (en)
DK (1) DK2445830T3 (en)
EA (1) EA027523B1 (en)
EG (1) EG26591A (en)
ES (1) ES2564655T3 (en)
MX (1) MX2011013913A (en)
MY (1) MY160806A (en)
PL (1) PL2445830T3 (en)
WO (1) WO2010149361A2 (en)
ZA (1) ZA201109421B (en)

Families Citing this family (19)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102011120938A1 (en) 2011-12-14 2013-06-20 Thyssenkrupp Uhde Gmbh Transportable reformer
DE102012015667A1 (en) 2012-08-09 2014-04-30 L'Air Liquide, Société Anonyme pour l'Etude et l'Exploitation des Procédés Georges Claude Discharge system for a steam reformer and storage for this
EP2708812B1 (en) * 2012-09-13 2017-08-02 L'AIR LIQUIDE, Société Anonyme pour l'Etude et l'Exploitation des Procédés Georges Claude Process and apparatus for endothermic reactions
US9843061B2 (en) 2013-04-05 2017-12-12 Panasonic Intellectual Property Management Co., Ltd. Hydrogen generator with a supplementary air flow rate adjustor for a combustor
CN103712230B (en) * 2013-12-21 2015-12-02 华中科技大学 A kind of built-in oxygen injection device for coal fired power generation oxygen-enriched combusting
CN104089279B (en) * 2014-07-08 2016-08-17 北京科电瑞通科技股份有限公司 Low nitrogen burning system
EP3153465B1 (en) * 2015-10-05 2020-01-01 L'Air Liquide Société Anonyme pour l'Etude et l'Exploitation des Procédés Georges Claude Reformer for producing synthesis gas
US11218418B2 (en) 2016-05-20 2022-01-04 Nutanix, Inc. Scalable leadership election in a multi-processing computing environment
EP3468707A1 (en) * 2016-06-09 2019-04-17 SABIC Global Technologies B.V. Systems for heating multi-tubular reactors
US11686471B2 (en) * 2017-06-14 2023-06-27 L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Apparatus for endothermic process with improved outer burners arrangement
CN107747868B (en) * 2017-08-25 2024-03-19 苏州南北深科智能科技有限公司 Combustion tower of solar silicon wafer sintering furnace
JP6944349B2 (en) * 2017-11-09 2021-10-06 エア・ウォーター株式会社 Hydrogen generator
CN110026133B (en) * 2018-01-11 2022-02-22 中国石化工程建设有限公司 Reforming furnace
CN109140427A (en) * 2018-09-30 2019-01-04 西安鑫顶天装备智能科技有限公司 A kind of combustion gas fission device
US11770447B2 (en) 2018-10-31 2023-09-26 Nutanix, Inc. Managing high-availability file servers
DE102019204814A1 (en) * 2019-04-04 2020-10-08 Thyssenkrupp Ag Reformer double floor
ES2941038T3 (en) * 2019-11-13 2023-05-16 Air Liquide Reformer furnace to carry out an endothermic process
US11768809B2 (en) 2020-05-08 2023-09-26 Nutanix, Inc. Managing incremental snapshots for fast leader node bring-up
CN114288967B (en) * 2021-12-10 2022-10-04 华中科技大学 Self-heating biomass gas catalytic reforming reactor, reforming system and method

Family Cites Families (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1484366A (en) * 1974-07-02 1977-09-01 Ici Ltd Methanol
GB8316588D0 (en) * 1983-06-17 1983-07-20 Ici Plc Contact material
US5417731A (en) * 1993-09-14 1995-05-23 Owens-Brockway Glass Container, Inc. Method of heating a charge, including injecting secondary oxidant into the output port
DE10333854A1 (en) 2003-07-24 2005-02-17 Uhde Gmbh Tubular cracking furnace used for reforming hydrocarbons e.g. to produce synthesis gas, comprises vertical cracker tubes, downward pointing burners and wedge shaped horizontal ceramic tunnels for removing flue gas
US7833009B2 (en) 2004-09-10 2010-11-16 Air Products And Chemicals, Inc. Oxidant injection method
ZA200507290B (en) * 2004-09-10 2006-06-28 Air Prod & Chem Oxidant injection method
DE102005021500A1 (en) 2005-05-10 2006-11-16 Uhde Gmbh Process for heating a steam / natural gas mixture in the region of a gas collecting pipe after a primary reformer
DE102007019830B3 (en) 2007-04-25 2008-07-31 Uhde Gmbh Reactor for catalytic primary reformation of hydrocarbons with water vapor under increased pressure, has device for top firring of reformation process furnace, and supply mechanism, which has main inlet channel and secondary inlet channel

Also Published As

Publication number Publication date
ES2564655T3 (en) 2016-03-28
DK2445830T3 (en) 2016-04-18
EG26591A (en) 2014-03-19
MX2011013913A (en) 2012-02-23
CN102459065A (en) 2012-05-16
EP2445830B1 (en) 2016-01-27
BRPI1015230A2 (en) 2017-07-04
ZA201109421B (en) 2012-11-28
CA2763108A1 (en) 2010-12-29
US20120126177A1 (en) 2012-05-24
EA201171314A1 (en) 2012-05-30
CN106395745A (en) 2017-02-15
CO6470869A2 (en) 2012-06-29
EA027523B1 (en) 2017-08-31
WO2010149361A2 (en) 2010-12-29
WO2010149361A3 (en) 2011-03-17
PL2445830T3 (en) 2016-07-29
US8882866B2 (en) 2014-11-11
EP2445830A2 (en) 2012-05-02

Similar Documents

Publication Publication Date Title
MY160806A (en) Primary reformer for reduced nitric oxide formation
US10647573B2 (en) Reformer device comprising a CO2 membrane
SA520412156B1 (en) System and Process for Synthesis Gas Production
RU2015150594A (en) METHOD AND SYSTEM FOR PRODUCING SYNTHESIS GAS USING A REFORMING SYSTEM BASED ON OXYGEN TRANSFER MEMBRANE WITH SECONDARY REFORMING
MX2014007063A (en) Transportable reformer.
Damanabi et al. Potential of tri-reforming process and membrane technology for improving ammonia production and CO2 reduction
US8728417B2 (en) Steam reforming furnace using porous burners
ZA201806973B (en) Co rich synthesis gas production
JP2009535292A (en) Reactor and method for carrying out reaction using hydrogen as reaction product
KR101526945B1 (en) Cylindrical Steam reformer using multi-tube
CN113574010A (en) Reforming furnace
US10773230B2 (en) Reformer for producing synthesis gas having improved burner waste gas flow
CN106560441A (en) Steam Reformer For Producing Synthesis Gas
RU2615768C1 (en) Reactor for catalytic steam and steam-carbon-dioxide hydrocarbon conversion
RU2020136497A (en) REFORMING FURNACE FOR ENDOTHERMAL PROCESS
NZ760482A (en) Method for improving efficiency of an ammonia synthesis gas plant
CN118973950A (en) Method and system for producing synthesis gas from various carbon and hydrogen sources by means of oxygen flame
JP4702771B2 (en) Steam reformer and steam reforming method
JP5339547B2 (en) Energy self-supporting lower hydrocarbon direct cracking process system
PL217503B1 (en) Reactor for the catalytic semi-combustion of natural gas